JPH0559079B2 - - Google Patents
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- Publication number
- JPH0559079B2 JPH0559079B2 JP63093996A JP9399688A JPH0559079B2 JP H0559079 B2 JPH0559079 B2 JP H0559079B2 JP 63093996 A JP63093996 A JP 63093996A JP 9399688 A JP9399688 A JP 9399688A JP H0559079 B2 JPH0559079 B2 JP H0559079B2
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- JP
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- Prior art keywords
- heat
- temperature
- fermentation
- mycelium
- fertilizer
- Prior art date
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Classifications
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F11/00—Other organic fertilisers
- C05F11/08—Organic fertilisers containing added bacterial cultures, mycelia or the like
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Fertilizers (AREA)
Description
(産業上の利用分野)
この発明は菌糸体肥料及びその製法に係り、そ
の目的は、農作物が生育する土壌中に埋設してお
くと、多孔質担体に担持された耐熱放線菌がその
系内において確実に育成され、その代謝産物であ
る植物ホルモンや各種ビタミン、分解物等が施用
した土壌や農作物等の栄養物として長期にわたつ
て作用されるとともに、多孔質担体のPHによつ
て、酸性土壌を中和させることができ、作物の成
長を効果的に促進させることのできる菌糸体肥料
及びこの菌糸体肥料の製法を提供することにあ
る。
(従来技術及びその問題点)
従来から有機物を醗酵させて肥料として使用す
るという技術はよく知られている。
例えば特公昭45−11535号公報に開示された
「土壌改良剤の製造方法」、更には、特開昭48−
26552号公報に開示された、「鶏糞の醗酵処理方
法」、或いは特開昭52−50874号公報に開示され
た、「肥効を伴う土壌改良剤の製造方法」等が知
られている。
これらは、いずれも有機物を醗酵させて、一部
未分解の有機物と分解された有機物と醗酵によつ
て生じた菌糸体との混合物を肥料として使用しよ
うという技術である。
これらは、古来から伝承されている堆肥と類似
の技術を経験的に応用したものである。
これらに加えて、特公昭62−31037号公報に
「土壌改良材」、特開昭54−66259号公報に「水溶
性の肥効促進剤を吸着させた土壌改良材」、更に、
特開昭54−111461号公報に「土壌改良材並びにそ
の製造法」がそれぞれ開示されている。
特公昭62−31037号公報に開示の「土壌改良材」
は、ゼオライトからなる培養基体に有機質栄養源
を付加するとともに糸状菌類、酵母菌類、細菌類
などの有用微生物又は胞子等を接種培養し、水分
補給状態下で加熱処理して醗酵させる技術であ
る。
特開昭54−66259号公報に開示の「水溶性の肥
効促進剤を吸着させた土壌改良材」は、連続多孔
質の無機質鉱物を吸着母体として、この吸着母体
に肥効促進剤溶液を含浸を含液させてなる水溶性
の肥効促進剤である。
又、特開昭54−111461号公報に開示されている
「土壌改良材並びにその製造法」は、粉砕ゼオラ
イト中に土壌細菌、好気性細菌等の微生物懸濁液
を含浸してなる土壌改良材である。
これら既開示の技術は、ゼオライト等の無機質
多孔質単体を用いてなるもので、そのPHが中性で
あり、日本に多い酸性土壌の改良にはあまり貢献
せず、また有害性があつたり、植物の成育に害の
ある微生物が担持されている場合もあるなどの問
題が存在した。
従つて、場合によれば既開示の醗酵肥料が植物
に対し、肥料効果を十分に発揮しないばかりか逆
に悪影響を及ぼすような場合もあり、係る場合に
従来特にその原因分析例えば醗酵条件、菌糸体の
菌の種類の分析、その他の原因解明が行われるこ
となく、単に醗酵の程度が低い等という経験的理
由で判断されていた。
さらに、特公昭47−25115号公報には、粒度を
調整した活性炭を鶏糞等の家畜の排泄物に添加し
てなる「鶏糞等の処理方法」が、また特開昭58−
36996号公報には、各種汚泥及び畜糞中に石炭粉、
木炭粉等を添加してコンポスト化する「汚泥及び
畜糞等の処理方法」が開示されている。
一方、特開昭57−17490号公報には、家畜や人
のし尿や鶏糞に、サーモアクチノミセス属等の耐
熱放線菌を接種し、培養させてなる「堆厩肥の製
造方法」が開示されている。
(発明の解決課題)
しかしながら、前記した特公昭47−25115号公
報及び特開昭58−36996号公報には、植物の成長
に寄与する耐熱放線菌を良好に生育させることの
できる環境については、何ら一切開示されておら
ず、しかも植物の成長促進とともに、日本に多く
存在する酸性土壌を中和させる等、土壌の性状を
改良するような作用を有する「肥料」については
何ら開示されていなかつた。
また、特開昭57−17490号公報には、耐熱放線
菌を人工的に接種して、培養し、肥料とする技術
が開示されているが、耐熱放線菌の最適な生育環
境という点については何ら開示されていない。
すなわち、この開示技術では、予め耐熱放線菌
を接種、培養させ、その期間において得られた耐
熱放線菌やその代謝産物を肥料として利用するも
のであるから、施用後の土壌中において耐熱放線
菌を育成させ、長期間その代謝産物等の栄養源を
作物に作用させることができないといつた課題が
存在した。
またこの開示技術には、植物の育成促進ととも
に、施用土壌の改良等に有効に作用されないとい
う課題も存在した。
このような事情に鑑み、植物の成長に寄与する
耐熱放線菌が、土壌に埋設した状態においても良
好に生育され、その耐熱放線菌の代謝産物や分解
物等を作物の栄養源として長期間利用できるとと
もに、施用する土壌、特に日本に多い酸性土壌を
中和して、改良する作用をも併せもつた菌糸体肥
料及びその製法の創出が望まれていた。
(発明の解決手段)
即ち、この発明は糸状菌及び耐熱放線菌を主と
した微生物群集からなる菌糸体であつて、前記微
生物群集の中の少なくとも50%以上が耐熱放線菌
である菌糸体がPH7.5〜9.5及び粒度6〜30メツシ
ユとされる木炭、活性炭、石炭、コークス、活性
コークス、泥炭、バームキユライトの中から選択
された一種以上の炭素系多孔質担体に担持されて
なることを特徴とする菌糸体肥料及びPH7.5〜9.5
及び粒度6〜30メツシユとされる木炭、活性炭、
石炭、コークス、活性コークス、泥炭、バームキ
ユライトの中から選択された一種以上の炭素系多
孔質担体を70〜80重量部用い、この担体に、炭素
率15%以下で含水率が25〜60%の有機物を20〜30
重量部用いて混練し、この混練物を系内温度15℃
以上に維持できる雰囲気内に静置して系内温度を
一定に保持させながら発酵させ、この混練物の発
酵系内の温度上昇開始に伴つて前記系内の温度を
エアレーシヨンにより55〜80℃に維持しながら少
なくとも5日間醗酵させてなることを特徴とする
菌糸体肥料の製法を提供することにより上記課題
を解決する。
(作用)
耐熱放線菌が担持された多孔質担体を農作物が
生育する土壌中に埋設しておくと、土壌中であつ
ても多孔質担体中の耐熱放線菌が、水や空気の流
通によつて確実に育成され、その代謝産物である
ビタミンや植物ホルモン、及び分解物等が農作物
や土壌の栄養源として長期にわたつて作用すると
ともに、多孔質担体のPHによつて酸性土壌が中和
され、農作物の成長を好適に促進する。
(発明の構成)
以下この発明の実施例について詳細に説明す
る。
この発明で好適に使用できる耐熱放線菌とは放
線菌であつて、特に高温55〜80℃で生育できる耐
熱放線菌でラセン状菌等をいい、例えば
Thermoactinomyces vulgaris、
Thermomoactinomyces spora actinobifida
(white)等である。
耐熱放線菌をこの発明において菌糸体肥料の主
要成分とする理由は、耐熱放線菌には植物に有害
な作用を与える有害菌が極めて少ない。
更には、耐熱放線菌の代謝産物の中に植物成長
ホルモン、各種ビタミン等が有る。
耐熱放線菌が分解して窒素補給源となる。
耐熱放線菌は自己分解する際、ガス状で分解す
るものも有り、土中に窒素分が過剰に供給される
ことが少ないという理由にもとづくものである。
この発明において多孔質担体に菌糸体肥料を担
持させるが、この多孔質担体をPH7.5〜9.5望まし
くは8〜9とする理由は、有効に耐熱放線菌の生
育に適したPH域が7.5〜9.5望ましくは8〜9であ
るとともにPH7.5〜9.5では糸状菌、細菌等の菌の
生育を防止でき、菌糸体肥料中の耐熱放線菌を一
定量に維持できるからである。
この発明において担体を多孔質担体に限定する
理由は、菌糸体肥料の貯蔵中、或いは土壌施用時
に耐熱放線菌の生育必須成分である水と空気を保
持するためである。
係る多孔質担体の具体例としては、PHが7.5〜
9.5に維持できるものであれば、無機質炭素系の
多孔質担体も使用できる。
この発明において使用できる多孔質担体を例示
すれば、木炭、活性炭、石炭、コークス、活性コ
ークス、泥炭、バームキユライト、パーライト、
ベントナイト、発泡性ウレタン等の無機質、有機
質、合成樹脂等の発泡体が例示される。
この発明において耐熱放線菌からなる菌糸体と
は、耐熱放線菌が菌糸体中の微生物群集として
100%を占めるものが最も望ましいが、少なくと
も微生物群集として50%以上が耐熱放線菌である
菌糸体とされる。
その理由は、50%未満の耐熱放線菌である場合
には、有害菌である細菌、或いは糸状菌の繁殖が
土壌施用後に発生することがあり、係る場合に悪
い影響があり、少なくとも菌糸体中の微生物群集
中50%以上が耐熱放線菌である場合に土壌施用後
に耐熱放線菌の優生繁殖が確保でき、この発明の
初期の目的が達成できるからである。
次のこの発明に係る菌糸体肥料の好適な製造方
法について述べる。
この発明においてはPH7.5〜9.5で粒度が6〜30
メツシユの多孔質担体を使用するのが望ましい。
この発明においてPH7.5〜9.5と多孔質担体のPH
域を限定する理由は、前述の如く耐熱放線菌の好
適な生育PH域を菌糸体肥料の製造中及び保存中に
確保するものであつて、有害菌が多い糸状菌等は
PH7.5〜9.5望ましくは8〜9というアルカリ性条
件下において生育しにくいという理由に基づく。
この発明において、多孔質担体の粒度を6〜30
メツシユとする理由は、後記醗酵の際に、30メツ
シユを超える細かい多孔質担体の場合には醗酵温
度を40℃以上に維持することが難しく、この発明
の目的である耐熱放線菌の充分な生育が望めず、
逆に6メツシユ未満の粒が大きい多孔質担体にお
いては、製造時の取り扱いの繁雑性があり望まし
くないからである。
このような多孔質担体を70〜80重量部用いる理
由は、多孔質担体の量が70重量部未満の場合に
は、後記醗酵条件において有機物の未分解率が多
くなり望ましくないとともに80重量部を超えて使
用する場合には、有機物から供給される水分が醗
酵系全体における水分含有率として少なくなり好
適な醗酵温度が得られず、結局いずれの場合にも
好ましくないからである。
この発明においてはこの多孔質担体に炭素率15
%以下で含水率が25〜60%の有機物を20〜30重量
部用いて混練する。
この発明で炭素率15%以下の有機物と限定する
理由は、炭素率が15%を超える有機物の場合には
繊維質セルロース系の含有物が多くなり、その結
果セルラーゼの所要量が多くなり放線菌中セルラ
ーゼの生育が優生となり、この発明の初期目的を
達成できないと言うこの発明者らの実験的知得に
よるものである。
この発明において有機物の含水率を25〜60%と
限定する理由は、混練物の醗酵系の水分が有機物
からのみ供給されるとともに醗酵物系の水分が30
〜40%ないと、十分な耐熱放線菌の醗酵温度が得
られないからであり、逆に醗酵物系に40%を超え
る含水率の場合や30%未満の場合には、いずれも
耐熱放線菌を醗酵させる十分な醗酵条件が得られ
ず好ましくないからである。
この発明において有機物を20〜30重量部使用す
る理由は、20重量部未満の場合は有機物の量が少
なすぎて各担体に対する菌糸体の生長が小さく、
各多孔質担体に対して均一に分散して菌糸体が付
着せず、逆に30重量部を超えて配合した場合に
は、菌糸体と多孔質担体との配合バランスがくず
れ菌糸体が過剰になつたり有機物の未分解率が多
くなり、いずれの場合も結局好ましくないからで
ある。
次いで、この混練物を系内温度15℃以上℃に維
持できる雰囲気内に静置する。
その理由は系内温度と外気温を遮蔽し、一定の
保温状態を保つことにより醗酵の均一性を保持す
るためである。
この温度が15℃以下の場合には、醗酵温度が十
分上がらず好ましくない。
系内温度を一定にし外気温と遮断した後、醗酵
物系の温度を55〜80℃望ましくは60〜70℃に維持
する。
醗酵温度が55℃以下の場合には醗酵を促進する
ために系内の15℃以上に維持された空気を一定時
間送りこみ醗酵温度を55から60℃に維持するが、
セルロース含量が炭素率15%以下の有機物を使用
するとして制限されしかも多孔質担体が多量に混
合されている含水率が制限されているという理由
で80℃以上に醗酵温度が上昇することは実際上お
こり得ない。
この状態で少なくとも5日間醗酵することによ
り耐熱放線菌からなる菌糸体であつて、この菌糸
体がPH7.5〜9.5の多孔質担体に担持されてなる菌
糸体肥料が製造される。
この発明においては醗酵期間は、少なくとも5
日間、望ましくは2〜3週間とするのがより望ま
しい。
尚、醗酵温度を55〜80℃に維持する理由は、55
℃未満では耐熱放線菌が初期目的の如く菌糸体群
集中の割合で得られず、逆に80℃を超える場合に
おいては嫌気性菌が生育するため、結局いずれの
場合も望ましくないからである。
この発明においては前述の如く炭素率15%以下
の有機物を20〜30重量部用いること、この有機物
の含水率を25〜60%と限定すること、更に多孔質
担体を70〜80重量部用いかつ粒度を6〜30メツシ
ユと限定することによつて醗酵温度が80℃以上に
なることがない。
したがつて通常の醗酵工程で行われる水を醗酵
物にかけて醗酵温度を下げるいわゆる切り返し工
程なくとも80℃以上に醗酵温度が上昇することが
ない。
(発明の効果)
以上詳述した如くこの発明に係る菌糸体肥料及
びその製法は糸状菌及び耐熱放線菌を主とした微
生物群集からなる菌糸体であつて、前記微生物群
集の中の少なくとも50%以上が耐熱放線菌である
菌糸体がPH7.5〜9.5及び粒度6〜30メツシユとさ
れる木炭、活性炭、石炭、コークス、活性コーク
ス、泥炭、バームキユライトの中から選択された
一種以上の炭素系多孔質担体に担持されてなるこ
とを特徴とする菌糸体肥料及びPH7.5〜9.5及び粒
度6〜30メツシユとされる木炭、活性炭、石炭、
コークス、活性コークス、泥炭、バームキユライ
トの中から選択された一種以上の炭素系多孔質担
体を70〜80重量部用い、この担体に炭素率15%以
下で含水率が25〜60%の有機物を20〜30重量部用
いて混練し、この混練物を系内温度15℃以上に維
持できる雰囲気内に静置して系内温度を一定に保
持させながら発酵させて、この混練物の発酵系内
の温度上昇開始に伴つて前記系内の温度をエアレ
ーシヨンにより55〜80℃に維持しながら少なくと
も5日間醗酵させてなることを特徴とする菌糸体
肥料の製法であるから、農作物の土壌中に埋設し
ておいても、多孔質担体に担持されている有益菌
の多い耐熱放線菌が、その系内で確実に育成さ
れ、その代謝産物である植物ホルモンや各種ビタ
ミン、或いは分解物である窒素源等を土壌や植物
の栄養源として長期間作用させることができると
ともに、この肥料を施用した酸性土壌に対して、
中和作用を発揮し、植物に対すると同時にその土
壌に対しても作用して、植物の成長を効果的に促
進させることができるという優れた効果を奏す
る。
以下この発明の実施例を記載することにより、
この発明の効果を一層明確にする。
(実施例 1)
多孔質担体としてPHが8.2で粒度が25メツシユ
パス、内部表面積が200m2/gのヤシガラ炭を70
重量部用いた。
この多孔質担体にPH8.8、含水率32.9%、炭素
率9.6%の鶏糞を25重量部用い、両者を混練した。
この混練物を醗酵槽内に静置し、醗酵槽内を25
℃に維持した。
この混練物の醗酵中の温度を測定し、温度の上
昇開始時及び混練物の醗酵中の温度が55℃以下に
なると、系内の空気をポンプにより、醗酵物中に
直接供給し、立ち上げ時は一気に温度を上昇させ
その他は温度を一定に管理した。
醗酵工程を通じて、醗酵物系中の温度が80℃以
上に上昇することはなかつた。
(組成分析)
この醗酵停止後、菌糸体肥料を組成分析したと
ころPH8.9、窒素全量1.65%、純蛋白質5.8%、ビ
タミンB10.01mg%、ビタミンB20.06mg%、パント
テン酸0.17mg%、ニコチン酸アミド0.30mg%であ
つた。
(菌糸体肥料中の菌の特定)
菌糸体中の菌を確定するために、直径9cm、深
さ1.5cmのペトリ皿4枚を用い、寒天と蒸留水か
らなる培地を充填し、前記菌糸体粒をペトリ皿1
〜3のそれぞれのペトリ皿1枚に対し、20粒均等
間隔で接種した。
尚、比較例としてペトリ皿4を25メツシユパス
で未処理のヤシガラ炭粒をそのまま用いて他のペ
トリ皿と同様に処理した。
このペトリ皿1〜4を25℃で4日間培養した
後、放線菌、糸状菌を発生したコロニー数で分類
分析した。
尚、この培養に際し培地は予め120℃、1気圧
下で20分間オート・クレイブで殺菌した。
この結果、ペトリ皿1は、試料粒1に対し、平
均して耐熱放線菌は7.4コロニー存在したに対し
糸状菌は5.0コロニーであつた。
ペトリ皿2においては、試料粒1に対し、耐熱
放線菌は平均4.2コロニー、糸状菌は1.8コロニ
ー、ペトリ皿3においては、試料粒1に対し、耐
熱放線菌は平均2.0コロニー、糸状菌は0.04コロ
ニーであつた。
このうち耐熱放線菌としてはラセン状菌が優先
しており、糸状菌においてはCladosporium属、
Penicillium属、Nigrospora属が見出された。
これら糸状菌のうちCladosporium属のものと
Penicillium属は比較例として用いたヤシガラ活
性炭粒のみのペトリ皿からも見られることからこ
れらは空中からの混入菌であると考えられ、実質
的に菌糸体肥料の微生物群集は耐熱放線菌が優先
しているものであつた。
次にこのような耐熱放線菌を使用した、施用例
について記載する。
尚、試験に際しては実施例1のみではなく、第
1表にしめす如く担体の種類を種々採用し、また
有機物を種々変化させた実施例及び比較例を使用
したが、これらの醗酵条件は実施例1と全く同様
に処理した。
(Industrial Application Field) The present invention relates to a mycelium fertilizer and a method for producing the same.The purpose of the invention is to allow heat-resistant actinomycetes supported on a porous carrier to enter the system when buried in the soil where agricultural crops grow. The metabolites, such as plant hormones, various vitamins, and decomposed products, act as nutrients for the applied soil and crops over a long period of time. To provide a mycelium fertilizer capable of neutralizing soil and effectively promoting the growth of crops, and a method for producing this mycelium fertilizer. (Prior art and its problems) The technology of fermenting organic matter and using it as fertilizer is well known. For example, ``Method for producing soil conditioner'' disclosed in Japanese Patent Publication No. 45-11535,
Known methods include the ``Method for Fermenting Chicken Manure'' disclosed in Japanese Patent Publication No. 26552, and the ``Method for Producing a Soil Conditioning Agent with Fertilizing Effect'' disclosed in JP-A-52-50874. All of these techniques involve fermenting organic matter and using a mixture of partially undecomposed organic matter, decomposed organic matter, and mycelium produced by fermentation as fertilizer. These are the empirical applications of techniques similar to composting, which have been passed down from ancient times. In addition to these, Japanese Patent Publication No. 62-31037 describes a "soil improvement material," Japanese Patent Publication No. 54-66259 describes a "soil improvement material adsorbed with a water-soluble fertilizer effect promoter," and furthermore,
``Soil improvement material and method for producing the same'' are disclosed in Japanese Patent Application Laid-open No. 111461/1983. "Soil improvement material" disclosed in Special Publication No. 62-31037
This is a technology in which an organic nutrient source is added to a culture substrate made of zeolite, and useful microorganisms such as filamentous fungi, yeast fungi, and bacteria or spores are inoculated and cultured, and the mixture is heated and fermented under hydrated conditions. ``Soil improvement material adsorbing a water-soluble fertilizer accelerator'' disclosed in JP-A-54-66259 uses a continuous porous inorganic mineral as an adsorption matrix, and a fertilizer accelerator solution is applied to this adsorption matrix. It is a water-soluble fertilizer effect promoter made by impregnating it with liquid. In addition, ``Soil improvement material and method for producing the same'' disclosed in Japanese Patent Application Laid-Open No. 111461/1987 is a soil improvement material obtained by impregnating a suspension of microorganisms such as soil bacteria and aerobic bacteria in crushed zeolite. It is. These previously disclosed technologies use a simple inorganic porous material such as zeolite, which has a neutral pH, does not contribute much to improving the acidic soil that is common in Japan, and is also harmful. There were problems, such as the fact that they sometimes carried microorganisms that were harmful to plant growth. Therefore, depending on the case, the disclosed fermented fertilizers may not only not exhibit sufficient fertilizer effects on plants, but may even have an adverse effect on plants. Without analyzing the type of bacteria in the body or elucidating other causes, the judgment was simply based on empirical reasons such as a low degree of fermentation. Furthermore, Japanese Patent Publication No. 47-25115 discloses a ``method for treating chicken manure, etc.'' in which activated carbon with adjusted particle size is added to livestock excrement such as chicken manure.
Publication No. 36996 states that coal powder,
A ``method for treating sludge, livestock excrement, etc.'' is disclosed, in which charcoal powder and the like are added to compost. On the other hand, JP-A No. 57-17490 discloses a ``method for producing compost'' in which heat-resistant actinomycetes such as Thermoactinomyces are inoculated and cultured in livestock or human excrement or chicken manure. There is. (Problem to be solved by the invention) However, the above-mentioned Japanese Patent Publication No. 47-25115 and Japanese Patent Application Laid-open No. 58-36996 describe an environment in which heat-resistant actinomycetes that contribute to plant growth can be grown well. There was no disclosure whatsoever about ``fertilizer,'' which has the effect of promoting plant growth and improving soil properties, such as neutralizing the acidic soil that exists in much of Japan. . Furthermore, JP-A-57-17490 discloses a technique for artificially inoculating heat-resistant actinomycetes, culturing them, and using them as fertilizer; however, regarding the optimal growth environment for heat-resistant actinomycetes, Nothing has been disclosed. That is, in this disclosed technology, heat-resistant actinomycetes are inoculated and cultured in advance, and the heat-resistant actinomycetes and their metabolites obtained during that period are used as fertilizer. There was a problem in that it was not possible to grow crops and provide nutrients such as metabolites to the crops for a long period of time. Further, this disclosed technology has the problem that it does not effectively promote plant growth and improve the soil to which it is applied. In view of these circumstances, heat-resistant actinomycetes that contribute to plant growth can grow well even when buried in soil, and the metabolites and decomposition products of heat-resistant actinomycetes can be used as nutritional sources for crops for a long period of time. It has been desired to create a mycelial fertilizer and a method for producing the same, which also has the ability to neutralize and improve the soil to which it is applied, especially the acidic soil that is common in Japan. (Means for Solving the Invention) That is, the present invention provides a mycelium consisting of a microbial community mainly consisting of filamentous fungi and heat-resistant actinobacteria, wherein at least 50% of the microbial community is heat-resistant actinobacteria. Supported on one or more carbon-based porous carriers selected from charcoal, activated carbon, coal, coke, activated coke, peat, and vermucilleite with a pH of 7.5 to 9.5 and a particle size of 6 to 30 mesh. Mycelium fertilizer and PH7.5-9.5 characterized by
and charcoal, activated carbon, with a particle size of 6 to 30 mesh,
Using 70 to 80 parts by weight of one or more types of carbon-based porous carrier selected from coal, coke, activated coke, peat, and vermucillite, this carrier has a carbon content of 15% or less and a moisture content of 25 to 60%. 20-30% organic matter
parts by weight, and the kneaded product is heated to an internal temperature of 15°C.
The kneaded product is left to ferment while maintaining the system temperature at a constant temperature in an atmosphere that can be maintained at a constant temperature, and as the temperature in the fermentation system of this kneaded product starts to rise, the temperature in the system is raised to 55 to 80 °C by aeration. The above-mentioned problem is solved by providing a method for producing a mycelium fertilizer, which is characterized in that it is fermented for at least 5 days while maintaining the mycelium. (Function) If a porous carrier carrying heat-resistant actinomycetes is buried in the soil where agricultural crops grow, the heat-resistant actinomycetes in the porous carrier will be absorbed by the circulation of water and air even in the soil. The metabolites such as vitamins, plant hormones, and decomposition products act as nutrients for crops and soil over a long period of time, and the pH of the porous carrier neutralizes acidic soil. , suitably promotes the growth of agricultural crops. (Structure of the Invention) Examples of the present invention will be described in detail below. Heat-resistant actinomycetes that can be suitably used in this invention are actinomycetes, and in particular heat-resistant actinomycetes that can grow at high temperatures of 55 to 80°C, such as spiral-shaped bacteria, such as
Thermoactinomyces vulgaris,
Thermoactinomyces spora actinobifida
(white) etc. The reason why heat-resistant actinomycetes are used as the main component of the mycelium fertilizer in this invention is that heat-resistant actinomycetes contain extremely few harmful bacteria that have harmful effects on plants. Furthermore, among the metabolic products of heat-resistant actinomycetes, there are plant growth hormones and various vitamins. Heat-resistant actinomycetes decompose and become a nitrogen supply source. This is based on the fact that when heat-resistant actinomycetes self-decompose, some decompose in a gaseous state, so that excessive nitrogen content is rarely supplied to the soil. In this invention, mycelial fertilizer is supported on a porous carrier, and the reason why this porous carrier is set to have a pH of 7.5 to 9.5, preferably 8 to 9, is because the pH range that is effectively suitable for the growth of heat-resistant actinomycetes is 7.5 to 9.5. 9.5 is preferably 8 to 9, and a pH of 7.5 to 9.5 is because growth of fungi such as filamentous fungi and bacteria can be prevented and the amount of heat-resistant actinomycetes in the mycelium fertilizer can be maintained at a constant level. The reason why the carrier is limited to a porous carrier in this invention is to retain water and air, which are essential components for the growth of heat-resistant actinomycetes, during storage of mycelium fertilizer or when applied to soil. Specific examples of such porous carriers include those with a pH of 7.5 to
An inorganic carbon-based porous carrier can also be used as long as it can maintain a value of 9.5. Examples of porous carriers that can be used in this invention include charcoal, activated carbon, coal, coke, activated coke, peat, vermquilite, perlite,
Examples include foams made of inorganic materials such as bentonite and foamable urethane, organic materials, and synthetic resins. In this invention, a mycelium consisting of heat-resistant actinomycetes refers to heat-resistant actinomycetes as a microbial community in the mycelium.
The most desirable one is one that accounts for 100%, but at least 50% of the microbial community is mycelium made up of heat-resistant actinomycetes. The reason for this is that if less than 50% of the heat-resistant actinomycetes are present, harmful bacteria or filamentous fungi may propagate after application to the soil, which may have a negative effect, at least in the mycelium. This is because when 50% or more of the microbial population concentration is heat-resistant actinomycetes, eugenic propagation of heat-resistant actinomycetes can be ensured after soil application, and the initial objective of this invention can be achieved. Next, a preferred method for producing the mycelium fertilizer according to the present invention will be described. In this invention, the pH is 7.5 to 9.5 and the particle size is 6 to 30.
Preferably, a mesh porous carrier is used. In this invention, PH7.5 to 9.5 and the PH of the porous carrier
The reason for limiting the range is to ensure a suitable growth pH range for heat-resistant actinomycetes during production and storage of mycelium fertilizer, as mentioned above, and to limit filamentous fungi, etc., which have many harmful bacteria.
This is because it is difficult to grow under alkaline conditions with a pH of 7.5 to 9.5, preferably 8 to 9. In this invention, the particle size of the porous carrier is 6 to 30.
The reason for using mesh is that during the fermentation described below, it is difficult to maintain the fermentation temperature at 40°C or higher in the case of fine porous carriers with more than 30 mesh, which is the purpose of this invention. I can't hope for
On the other hand, a porous carrier having large grains of less than 6 meshes is undesirable because it requires complicated handling during production. The reason why such a porous carrier is used in an amount of 70 to 80 parts by weight is that if the amount of the porous carrier is less than 70 parts by weight, the undecomposed rate of organic matter will increase under the fermentation conditions described later, which is not desirable. This is because if it is used in excess of this amount, the moisture supplied from the organic matter will decrease as a moisture content in the entire fermentation system, making it impossible to obtain a suitable fermentation temperature, which is ultimately undesirable in either case. In this invention, this porous carrier has a carbon content of 15
% or less and a water content of 25 to 60% by weight. The reason why this invention is limited to organic substances with a carbon content of 15% or less is that organic substances with a carbon content of more than 15% contain a large amount of fibrous cellulose, and as a result, the required amount of cellulase increases, resulting in actinomycetes. This is based on the experimental knowledge of the inventors that the growth of medium cellulase becomes eugenic and the initial purpose of this invention cannot be achieved. The reason why the moisture content of organic matter is limited to 25 to 60% in this invention is that the moisture in the fermentation system of the kneaded product is supplied only from the organic matter, and the moisture content in the fermentation product system is 30%.
This is because if the moisture content is less than ~40%, sufficient fermentation temperature for heat-resistant actinomycetes cannot be obtained, and conversely, if the moisture content of the fermentation product exceeds 40% or is less than 30%, heat-resistant actinomycetes This is because sufficient fermentation conditions cannot be obtained for fermentation, which is not preferable. The reason why 20 to 30 parts by weight of organic matter is used in this invention is that if it is less than 20 parts by weight, the amount of organic matter is too small and the growth of mycelium on each carrier is small.
If the mycelium is not evenly dispersed and attached to each porous carrier, and on the other hand is added in excess of 30 parts by weight, the balance between the mycelium and the porous carrier will be disrupted, resulting in excessive mycelium. This is because the undecomposed rate of organic matter increases, which is ultimately undesirable in either case. Next, this kneaded product is left to stand in an atmosphere where the system internal temperature can be maintained at 15°C or higher. The reason for this is to maintain the uniformity of fermentation by shielding the temperature inside the system from the outside temperature and maintaining a constant heat retention state. If this temperature is below 15°C, the fermentation temperature will not rise sufficiently, which is not preferable. After keeping the temperature inside the system constant and insulating it from the outside temperature, the temperature of the fermented product system is maintained at 55-80°C, preferably 60-70°C. If the fermentation temperature is below 55℃, air maintained at 15℃ or above is pumped into the system for a certain period of time to promote fermentation, and the fermentation temperature is maintained at 55 to 60℃.
In practice, the fermentation temperature does not rise above 80℃ because the cellulose content is limited by using organic matter with a carbon content of 15% or less, and the moisture content is limited by mixing a large amount of porous carrier. It can't happen. By fermenting in this state for at least 5 days, a mycelium fertilizer made of heat-resistant actinomycetes supported on a porous carrier having a pH of 7.5 to 9.5 is produced. In this invention, the fermentation period is at least 5
It is more desirable to set it as several days, desirably 2 to 3 weeks. The reason for maintaining the fermentation temperature at 55-80℃ is 55
This is because if the temperature is below 80°C, heat-resistant actinomycetes cannot be obtained at the concentration of mycelium as initially desired, and on the other hand, if the temperature exceeds 80°C, anaerobic bacteria will grow, which is ultimately undesirable in either case. In this invention, as mentioned above, 20 to 30 parts by weight of an organic material with a carbon content of 15% or less is used, the water content of this organic material is limited to 25 to 60%, and furthermore, 70 to 80 parts by weight of a porous carrier is used. By limiting the particle size to 6 to 30 mesh, the fermentation temperature will not exceed 80°C. Therefore, the fermentation temperature does not rise above 80°C even without the so-called cut-back process, which is performed in a normal fermentation process, in which water is poured over the fermented material to lower the fermentation temperature. (Effects of the Invention) As detailed above, the mycelium fertilizer and the method for producing the same according to the present invention is a mycelium consisting of a microbial community mainly consisting of filamentous fungi and heat-resistant actinomycetes, and at least 50% of the microbial community is The above are heat-resistant actinomycetes.Mycelia have a pH of 7.5 to 9.5 and a particle size of 6 to 30 mesh, and are made of one or more types of carbon selected from charcoal, activated carbon, coal, coke, activated coke, peat, and vermquilite. A mycelium fertilizer characterized by being supported on a porous carrier, and charcoal, activated carbon, coal, which has a pH of 7.5 to 9.5 and a particle size of 6 to 30 mesh.
Use 70 to 80 parts by weight of one or more types of carbon-based porous carrier selected from coke, activated coke, peat, and vermquilite, and add organic matter to this carrier with a carbon content of 15% or less and a water content of 25 to 60%. 20 to 30 parts by weight of the kneaded product is kneaded, and the kneaded product is allowed to stand in an atmosphere where the system temperature can be maintained at 15°C or higher, and fermented while maintaining the system internal temperature at a constant level. This method of producing mycelial fertilizer is characterized by fermenting for at least 5 days while maintaining the temperature in the system at 55 to 80°C by aeration as the temperature in the system starts to rise. Even if it is buried, the heat-resistant actinomycetes, which are many beneficial bacteria supported on the porous carrier, will be reliably grown within the system, and their metabolites such as plant hormones and various vitamins, as well as decomposed products of nitrogen, will be grown within the system. This fertilizer can act as a nutrient source for soil and plants for a long period of time, and it can also be applied to acidic soil.
It exhibits a neutralizing effect, acts on plants as well as on the soil thereof, and has the excellent effect of effectively promoting plant growth. By describing examples of this invention below,
The effects of this invention will be made clearer. (Example 1) Coconut husk charcoal with a pH of 8.2, a particle size of 25 mesh, and an internal surface area of 200 m 2 /g was used as a porous carrier.
Parts by weight were used. 25 parts by weight of chicken manure having a pH of 8.8, a water content of 32.9%, and a carbon content of 9.6% were used in this porous carrier, and both were kneaded. This kneaded material was left standing in the fermentation tank, and the inside of the fermentation tank was heated to 25°C.
It was maintained at ℃. The temperature during fermentation of this kneaded product is measured, and when the temperature starts to rise and the temperature during fermentation of the kneaded product falls below 55℃, air in the system is supplied directly into the fermented product using a pump to start up the fermentation. At times, the temperature was raised all at once, and at other times, the temperature was kept constant. Throughout the fermentation process, the temperature in the fermentation product system did not rise above 80°C. (Composition analysis) After stopping this fermentation, the composition of the mycelial fertilizer was analyzed and found to be PH8.9, total nitrogen 1.65%, pure protein 5.8%, vitamin B 1 0.01 mg%, vitamin B 2 0.06 mg%, pantothenic acid 0.17 mg% , nicotinic acid amide 0.30 mg%. (Identification of bacteria in mycelium fertilizer) In order to determine the bacteria in mycelium, four Petri dishes with a diameter of 9 cm and a depth of 1.5 cm were filled with a medium consisting of agar and distilled water, and the mycelium was Place grains in Petri dish 1
20 seeds were inoculated evenly spaced into one Petri dish of ~3. As a comparative example, Petri dish 4 was treated in the same manner as the other Petri dishes using untreated coconut shell charcoal grains for 25 mesh passes. After culturing these Petri dishes 1 to 4 at 25° C. for 4 days, they were classified and analyzed based on the number of colonies that generated actinobacteria and filamentous fungi. During this culture, the medium was sterilized in advance in an autoclave at 120°C and 1 atm for 20 minutes. As a result, in Petri dish 1, there were on average 7.4 colonies of heat-resistant actinomycetes and 5.0 colonies of filamentous fungi per sample particle 1. In Petri dish 2, an average of 4.2 colonies of heat-resistant actinomycetes and 1.8 colonies of filamentous fungi per sample grain 1, and in Petri dish 3, an average of 2.0 colonies of heat-resistant actinomycetes and 0.04 colonies of filamentous fungi per sample grain 1. It was a colony. Among these, the heat-resistant actinomycetes are dominated by spiral-shaped bacteria, and among filamentous fungi, Cladosporium spp.
Genus Penicillium and Nigrospora were found. Among these filamentous fungi, those of the genus Cladosporium
Since the genus Penicillium was also found in the Petri dish containing only coconut shell activated carbon grains used as a comparative example, these are considered to be contaminants from the air, and the microbial community of mycelium fertilizer is essentially dominated by heat-resistant actinomycetes. It was something that was happening. Next, application examples using such heat-resistant actinomycetes will be described. In addition, in the test, we used not only Example 1 but also Examples and Comparative Examples in which various types of carriers were adopted and organic substances were varied as shown in Table 1, but these fermentation conditions were the same as those in Example 1. It was treated in exactly the same manner as 1.
【表】
(施用例)
方法 1 試験の規模
ポツト試験(1/5000aポツト)
2 供試品目 コウライシバ
3 供試土壌 砂 土
4 試験時期 4月〜10月
5 試験区別
対照区 3ポツト
各実施例区 土壌中10%施用各3ポツト
土壌中20%施用各3ポツト
各比較例区 土壌中10%施用各3ポツト
土壌中20%施用各3ポツト
加えて、普通化成肥料3gをそれぞれのポツト
に施用した。
尚、供試土壌は粗砂90.1%、細砂9.0%、シル
ト0.0%、粘土0.9%、塩基置換容量0.44me/100
g、PH6.8であつた。
6ケ月後の茎の重量を測定した。それぞれの平
均値をまとめて、第2表に記す。[Table] (Application example) Method 1 Test scale
Pot test (1/5000a pot) 2. Test item: Orifolia 3. Test soil: Sand Soil 4. Test period: April to October 5. Test classification: Control area: 3 pots Each example area: 10% in soil applied 3 pots each 20% in soil 3 pots each for application 3 pots each for 10% soil application 3 pots each for 20% soil application In addition, 3 g of ordinary chemical fertilizer was applied to each pot. The test soil was 90.1% coarse sand, 9.0% fine sand, 0.0% silt, 0.9% clay, and base replacement capacity 0.44me/100.
g, pH was 6.8. The weight of the stems was measured after 6 months. The respective average values are summarized and shown in Table 2.
【表】
以上の結果から明らかな如く、この発明に係る
菌糸体肥料は優れた効果を奏することが明らかで
ある。[Table] As is clear from the above results, it is clear that the mycelium fertilizer according to the present invention has excellent effects.
Claims (1)
からなる菌糸体であつて、前記微生物群集の中の
少なくとも50%以上が耐熱放線菌である菌糸体が
PH7.5〜9.5及び粒度6〜30メツシユとされる木
炭、活性炭、石炭、コークス、活性コークス、泥
炭、バームキユライトの中から選択された一種以
上の炭素系多孔質担体に担持されてなることを特
徴とする菌糸体肥料。 2 PH7.5〜9.5及び粒度6〜30メツシユとされる
木炭、活性炭、石炭、コークス、活性コークス、
泥炭、バームキユライトの中から選択された一種
以上の炭素系多孔質担体を70〜80重量部用い、こ
の担体に炭素率15%以下で含水率が25〜60%の有
機物を20〜30重量部用いて混練し、この混練物を
系内温度15℃以上に維持できる雰囲気内に静置し
て系内温度を一定に保持させながら発酵させ、こ
の混練物の発酵系内の温度上昇開始に伴つて前記
系内の温度をエアレーシヨンにより55〜80℃に維
持しながら少なくとも5日間醗酵させてなること
を特徴とする菌糸体肥料の製法。[Scope of Claims] 1. A mycelium consisting of a microbial community mainly consisting of filamentous fungi and heat-resistant actinomycetes, wherein at least 50% of said microbial community is heat-resistant actinomycetes.
Supported on one or more carbon-based porous carriers selected from charcoal, activated carbon, coal, coke, activated coke, peat, and vermucilleite with a pH of 7.5 to 9.5 and a particle size of 6 to 30 mesh. A mycelium fertilizer characterized by: 2 Charcoal, activated carbon, coal, coke, activated coke with a pH of 7.5 to 9.5 and a particle size of 6 to 30 mesh,
Use 70 to 80 parts by weight of one or more carbon-based porous carriers selected from peat and vermquilite, and add 20 to 30 parts by weight of organic matter with a carbon content of 15% or less and a moisture content of 25 to 60% to this carrier. The kneaded product is fermented while keeping the system temperature constant by standing in an atmosphere where the system internal temperature can be maintained at 15℃ or higher, and the kneaded product is fermented until the temperature in the fermentation system starts to rise. A method for producing a mycelial fertilizer, characterized in that fermentation is carried out for at least 5 days while maintaining the temperature in the system at 55 to 80°C by aeration.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9399688A JPH01264987A (en) | 1988-04-15 | 1988-04-15 | Mycelium fertilizer and production thereof |
| DE1989608936 DE68908936T2 (en) | 1988-04-15 | 1989-04-14 | Fungus fertilizers and process for their preparation. |
| EP19890106714 EP0337483B1 (en) | 1988-04-15 | 1989-04-14 | Mycelial fertilizer and a method of producing the same |
| US07/759,973 US5196042A (en) | 1988-04-15 | 1991-09-17 | Mycelial fertilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9399688A JPH01264987A (en) | 1988-04-15 | 1988-04-15 | Mycelium fertilizer and production thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01264987A JPH01264987A (en) | 1989-10-23 |
| JPH0559079B2 true JPH0559079B2 (en) | 1993-08-30 |
Family
ID=14098012
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9399688A Granted JPH01264987A (en) | 1988-04-15 | 1988-04-15 | Mycelium fertilizer and production thereof |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP0337483B1 (en) |
| JP (1) | JPH01264987A (en) |
| DE (1) | DE68908936T2 (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0777991B2 (en) * | 1991-01-23 | 1995-08-23 | 株式会社コーエー | Organic fermentation fertilizer and method for producing the same |
| DE4138883C1 (en) * | 1991-11-27 | 1993-05-27 | Hoechst Ag, 6230 Frankfurt, De | |
| JPH06157176A (en) * | 1992-04-10 | 1994-06-03 | Towa Kagaku Kk | Microbial fertilizer and production and utilization thereof |
| NL1000204C2 (en) * | 1995-04-24 | 1996-10-25 | Carbo Beheer B V | Method for improving chemical, physical and biological processes in agriculture, horticulture, animal husbandry and humans. |
| WO1997019902A1 (en) * | 1995-11-29 | 1997-06-05 | Kabushiki Kaisha Kingcoal | Mycelial fertilizer and process for producing the same |
| DE102013019294A1 (en) * | 2013-11-19 | 2015-05-21 | Carboverte Srl | Activated charcoal for soil improvement |
| JP6324042B2 (en) * | 2013-12-02 | 2018-05-16 | 株式会社キングコール | Mycelium fertilizer and its production method |
| JP6499340B1 (en) * | 2018-03-06 | 2019-04-10 | アヲハタ株式会社 | Composition for promoting plant growth and use thereof |
| JP6497720B1 (en) * | 2018-03-06 | 2019-04-10 | アヲハタ株式会社 | Composition for promoting plant growth and use thereof |
| WO2025046755A1 (en) * | 2023-08-29 | 2025-03-06 | 株式会社キングコール | Panama disease control agent for cavendish bananas and control method using same |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1817528A1 (en) * | 1968-12-31 | 1970-09-17 | Poschenrieder Dr Hanns | Organic fertilizers with delayed nitrogen release - for animal or vegetable wastes mixed with salts, sorptive fillers and aldehydes then incubating with actinomycetes animal vegetabl waste mixed salt sorption fill aldehyde incubate actinomycetes |
| US4077793A (en) * | 1977-03-28 | 1978-03-07 | Rudolf Krupicka | Composition for favoring germination and growth of the vegetable species and its application |
| JPS5466259A (en) * | 1977-10-25 | 1979-05-28 | Chuo Shizai Kk | Soil improving material adsorbed with water soluble fertilizer effect promotor and production thereof |
| JPS54111461A (en) * | 1978-02-17 | 1979-08-31 | Hiromichi Nakatsu | Soil improver and production thereof |
| JPS6231037A (en) * | 1985-08-02 | 1987-02-10 | Olympus Optical Co Ltd | Optical head |
| DE3644671C1 (en) * | 1986-12-30 | 1988-03-17 | Friedrich Gmbh & Co Bauservice | Fertilizer containing fungal mycelium and process for producing the fertilizer |
-
1988
- 1988-04-15 JP JP9399688A patent/JPH01264987A/en active Granted
-
1989
- 1989-04-14 EP EP19890106714 patent/EP0337483B1/en not_active Expired - Lifetime
- 1989-04-14 DE DE1989608936 patent/DE68908936T2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| EP0337483B1 (en) | 1993-09-08 |
| JPH01264987A (en) | 1989-10-23 |
| EP0337483A1 (en) | 1989-10-18 |
| DE68908936T2 (en) | 1994-02-24 |
| DE68908936D1 (en) | 1993-10-14 |
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